Method and apparatus for conditioning and supplying water and carbon dioxide to carbonators



Jun@ 22, 3.943,. E. GEERTZ ET AL 2,322,625

METHOD AND APPARATUS FOR CONDITONNG. AND SUPPLYING LS-Sheet WATER AND CARBON DIOXIDE TO CARBONATORS Filed Sept. ll 194].

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June 22, i943, E. GEERTZ ET AL 2,322,625

METHOD AND APPARATUS FOR CONDITIONING AND SUPPLYING WATER AND CARBON DIOXIDE TO CARBONATORS Filed Sepa. ll, 1941 3 Sheets-Sheet 2 .98 36g 70 50M/vom 1u/f Charles A Geiz O/v WA rm ffy/045.5

Nom/ALLY 105m Hfmy Im Lss 33M E( W 1 l Eric Geerzmzol June 22, 1943.l E GEERTZ ET AL 2,322,625

METHOD AND APPARATUS FOR CONDITIONING AND SUPPLYING WATER AND CARBON DIOXIDE TO CARBONATORS 3 Sheets-Sheet 3 Eric Geerz and '/uz'ZeSfL Getz Filed sept. 11, 1941 mqw Patented June 22, 1943 METHOD AND APPARATUS FOR CONDITION- ING AND SUPPLYIN G WATER AND CARBON DIOXIDE TO CARBONATORS Eric Geertz and Charles A. Getz, Glen Ellyn, Ill.,

assignors, by mesne assignments, to Reconstruction Finance Corporation, Chicago, Ill., a corporation of the United States Application September 11,1941, Serial No. 410,468

22 Claims.

This invention relates to methods of and apparatus forconditioning and supplying water and carbon dioxide to carbonators used in beverage bottling plants.

Present day plants engaged in the bottling of soft drinks and other beverages are operated on the principle of delivering to carbonators water, which is suitable for human consumption,at a substantially constant temperature which is just slightly above the freezing point. A very accurate control of the water temperature is necessary in order to obtain a constant, uniform maximum amount of carbonation. As the temperature of water obtained either from the city mains or from an artesian well is never at the desired low temperature at which the carbonators are operated, it is necessary to employ refrigeration Ifor the Water to obtain the necessary accurate control.

The carbon dioxide vapors used in the carbonators to produce the carbonated` water heretofore has been drawn from a suitable bank of commercial cylinders and delivered to the carbonators through suitable pressure regulators which will lower the high pressure always prevailing in the cylinders to the low operating pressure of the carbonators. It is as important to maintain an accurate control of the carbon dioxide pressure in the carbonatorsv as it is to maintain an accurate control of the water temperature. The carbon dioxide stored in the bank of cylinders is subjected to the temperature of the surrounding atmosphere and consequently the pressure of the Withdrawn vapors varies from season to season,`day to day, and even hour to hour. The Withdrawal of vapors from the cylinders, also, lowers the pressure of the remaining carbon dioxide and the more or less constant substitution of fully charged cylinders for exhausted ones results in varying the pressure of the withdrawn vapors. These constantly varying pressures prevailing in the discharge line from the bank of cylinders necessitates maintaining constant supervision over the pressure regulators or the desired uniform pressure will not be maintained in the carbonators.

The constant Withdrawal of nothing but carbon dioxide vapors from the bank of cylinders produces a self-cooling or self-refrigerating aotion which is applied to the liquid remaining in the cylinders. 4This action is caused by the evaporation of liquid in the cylinders to replace the vapors which are withdrawn. As the vapor pressure in the cylinders corresponds directly with the temperature of the liquid, this self-cooling or self-refrigeration of the liquid causes the vapor pressure to drop with the result that-the pressure regulators must be adjusted to compensate for this factor.

If the discharge of vapors from the cylinders continues for a sufficient length of time and at a suiciently rapid rate, the temperature of the remaining liquid will be lowered to the value at which the liquid will solidify. 'I'his temperature value is approximately 70 F. while the vapor pressure is approximately 75 pounds per square .inch, absolute. Naturally, it is impossible to ,Withdraw carbon dioxide vapors from cylinders f in which the remaining liquid has been solidifled.

Further discharge from cylinders aiected in this way cannot be obtained until sufficient heat has been absorbed from the surrounding atmosphere to cause sublimation of the solid carbon dioxide. Continuous discharge of approximately threequarters of a starting charge in a cylinder will result, in solidifying the remaining one-quarter.

The carbon dioxide vapors, in passing from the high pressure side to the low pressure side of the pressure regulators, are subjected to a throttling action which brings about a drop in temperature.

As the drop in temperature, resulting from throttling, is in direct proportion to the reduction in pressure, it is impossible to/deliver carbon dioxide vapors to carbonators at a constant temperature unless the pressures on both sides of the regulators are maintained at constant values. It will be appreciated that it is extremely dilcult to maintain a constant temperature for the vapors entering the carbonators when the vapor pressure on the high pressure side of /the regulators is almost constantly varying and through wide limits.

It was pointed out above that the carbon dioxide conlned in the usual commercial cylinders is constantly subjected ,to the varying tempratures of the surrounding atmosphere. The va.-

por pressure of the carbon dioxide in the commercial cylinders will fall between 854 pounds and 968 pounds per square inch, absolute, when the temperature of the surrounding atmosphere is between F. and 80 F. Although the vapor pressure maintained in the carbonators of different plants may vary, within certain limits, it is the usual practice to employ a pressure which falls below pounds per square inch. Therefore, pressure drops at the pressure regulators of from 700 pounds to 800 pounds will take place when the liquid carbon dioxide in the commercial cylinders is subjected to the comparatively common temperature range of from 70 F. to 80 F.

jsure and temperature control.

-The throttling effect produced by temperature dropsof from 700 pounds toI 800 pounds will cause the carbon dioxide vapors to be lowered to a temperature below 32 F. and will cause freezing of any water vapors passing through the pressure regulators with the carbon dioxide vapors.

The carbon dioxide vapors withdrawn from commercial cylinders very frequently contain some water vapors. Therefore, it is necessary to provide some form of preheating .means for superheating the vapors just before they are delivered to the pressure regulators or frozen water vapors will cause faulty operation of the regulators.

. ing carbon` dioxide liquid and vapors from the tanks .for delivery to the carbonators. Starting with ya vapor pressure in a lstorage tank which corresponds with the minimum vapor pressure or theaforementioned narrow range, liquid carbon dioxide is withdrawn from the tank -until the vapor pressure rises to the maximum value ofthe range, which rise will be caused by the absorption of heat through the insulation of the tank and the rise in temperature which results from this absorption. When the maximum pressure of the range is reached, the withdrawalis automatically changed over to vapor, and this type oi withdrawal continues until self-refrigeration, resultingfrom vaporization of liquid to take the place of the withdrawn vapors, again lowers the vapor pressure in the tank to the minimum value -of the range.

When this minimum value is' reached, the withdrawal i is automatically changed back toliquid. This cycle of alternately withdrawing vapors and liquid ls repeated as often as is necessary to maintain the desired pres- During prolonged shut down periods, such yas 4over week ends orholidays, of a bottling plant equipped with this type of carbon dioxide supply, the vapor pressure of the ystored liquid is prevented from rising above a preselected extreme pressure value, which may bear any desired relation tothe maximum value of the operating y pressure range, by refrigerating the stored liquid.

The methods and apparatus of the aforesaid application further operate on the principle oi' employing drinking water from city mains or suitable wells going to the carbonators as a source of heat for vaporizing the liquid carbon dioxide withdrawn from the storage tank and for heating the vapors thus formed as well as the vapors withdrawn directly from` the tank before they are delivered tothe pressure regulators in ad- Vance yof the loarbonators. This preheatlng of the vapors by the city or well water 4not only helps to lower the temperature of the water so that less refrigeration of the same is necessary, but also has the effect of preventing the throttling action, caused by pressure drop at the pressure regulators, from lowering the temperature of the vapors to 32F., or the temperature at whichv water vapors in the carbon dioxide will freeze.

The present inventionis in the nature oi' a modification of the invention covered by the aforesaid application. It, likewise, stores the liquid carbon dioxide in bulk in large capacity, heat insulated tanks at a preselected narrow range of subatmospheric temperatures and their corresponding vapor pressures. Additionally, it partiallycoolsthe city water going to the carbonators and raises the temperature of the carbon dioxide vapors, delivered to the pressure reg-- ulators in advance of the carbonators, by bringing the two iiuids in lieat exchange relation. The liquid in storage during prolonged shut down periods, also, is prevented from rising above any desired extreme pressure value by applying refrigeration thereto. a It is, however, the primary object of this invention to provide methods and apparatus for conditioning and supplying carbon dioxide vapors to carbonators of beverage bottling plants by withdrawing nothing but vapors from the bulk storage tanks and maintaining the liquid remaining in the tanks within the preselected narrow range of subatmospheric temperatures and their corresponding vapor pressures by applying heat,

in automatically controlled amounts, to the liquid to compensate for the self-refrigeration resulting from the withdrawal of vapors.

A further important object of the invention is to employ water from city mains, or some other suitable source, either with or without additional heat beingv appliedv thereto, as the medium for heating the stored liquid carbon dioxide to counteract the aforesaid self-refrigeration effect.

Still another object of the invention is to provide methods and apparatus for supplying the requiredv amount of water, at the desired constant low temperature, to carbonators for beverage bottling plants by employing the low tem-. l 'peraturedvapors discharged from the storage 40.

tank or the low temperature oi' the liquid remaining in the storage tank as means of refrigeration for the water. J

OtherA objects and advantages of the invention will be apparent during the course of the following description.

In the accompanying drawings forming a part of this speciiication and in which like numerals are employed to designate like parts throughout the same,

Figure l is a diagrammatic view of the apparatus of a beverage bottling plant which will Afunction to supply carbon dioxide vapors oi substantially constant pressure to the pressure regulators of carbonators and to supply the drinking water, at a constant temperature,to the wiring system with its automatic controls for said plant, which will accomplishthe same general objects as the apparatus of Fig. 1.

In the drawings, wherein for the purpose of illustration are shown the preferred embodiments of this invention. and ilrst particularly referring to Fig. 1, the reference character l designates a bulk storage tank which is completely enclosed within the relatively thick layer of insulating material 6. Of course, a suitable finishing sheathing or covering, not specifically illustrated, is applied to the exterior of the inaulation. The enclosing of the bulk storage tank `in insulating material is for the purpose of retarding the input of heat from the surround# .ing atmosphere. As no perfect insulation has been developed so far, heat will be absorbed by the carbon dioxide confined in the tank and this.

inch, This liquid ycarton dioxide will be charged inw the storage tank l from the proper transportation vehicle at a vapor pressure of approximately 300 pounds. The liquid spaces of `the storage tank 5 and the tank of the vehicle will be placed in communication by any suitable piping, which has not been shown, and -a suitable pump may be employed in this piping to accomplish the desired transfer of the liquid. The vapor spaces of the two tanks, also, .will be placed in open communicationwith each other. Fig. l

' discloses a'vapor draw oif line 8 for the tank 5 input of heat will bring about an increase in temperature and pressure of the stored carbon dioxide which will be helpfulto a limited extent in carrying out the desired objects of the invention. The bulk storage tank l may be provided with any desired capacity whichv is most suitable for the beverage bottling plant in which `the illustrated apparatus is installed. 'Ihe maximum capacity for any tank so far installed for the bulk storage of liquid carbon dioxide is 125 tons, but there is no known reason why larger capacities cannot be provided if desired.

f course, any desired lower capacity tank may be employed, and it has been determined that which 'leads to the exterior thereof and is provided with a branch line 9 that is employed durlng the charging of liquid carbon dioxide into the tank to connect the vapor space of this tank with the vapor space of the transportation vehicle. It` was explained above that theV re frigerating coil l, and a suitable commercial refrigerating machine which has not been-disclosed, are'employed for preventing the vapor pressurein the tank l from exceeding the preselected extreme maximum pressure value. If,

for some reason, the refrigerating machine is' renderedi'noperative, the vapor pressure in the tank 5 is prevented from exceeding said extreme maximum pressure value by means of suitable bleeder valves and safety discs, both not shown, which will operate to release carbon dioxide vapors and effect self-refrigeration of the remaining liquid. For example, if the -refrigerating f machine connected to the co'il 'I is provided with satisfactory if. the maximum pressure maintained in the tank doesA not `exceed approximately 300 pounds per square inch.

It will be assumed, therefore, that the tank l has a maximum safety pressurerating of 325 pounds per square inch and that the system will be operated so that the vapor pressure of the liquid carbon' dioxide stored in the tank will not l b'e permitted to exceed approximately 300 pounds per square inch. To. accomplish this desired result, a refrigerating coil 'I is located in the vapor space :of the tank'i andl is bonnected by the pipelines la to any standard make of mechanical refrigerating machine, not shown, which'has a sufficienti capacity for the particular tank involved. The function of this refrigerating coil 1 is to condense carbon dioxide vapors in the uppervapor space of the tank .l lo that the drops of condensation may be returned, by gravity, to they liquid in the lower party of the tank. l

As the carbon dioxide is withdrawn from the tank I for use in the bottling plant, the supply of carbon dioxide is replenished in any desired manner. Thereis available at this time a carbon dioxide distribution system which embodies thejtransportation of liquid carbon dioxide in a suitable automatic control device which will cause the machine to operate when'the vapor pressure in the tank I reaches an extreme maximum value of 300 pounds per square inch, oneorl more bleeder valves may be provided and set for operationl at slightly higher values; for example, at 5 pound pressure increases. If we assume that two bleeder valves are provided which will operate respectively at 305 pounds and 310 pounds, these valves will only perform their intended 'functions incase the refrigerator plant fails to operate when the vapor pressure in the tank reaches 300 pounds. 'Iwo or more bleeder valves are employed and set for operation at relatively higher values so that, for example, the

valve set at 310 pounds will only .operate in case the valve set for-305 pounds fails. A safety or rupturable disc is employed as the final or ultimate safety device. This disc will blow out if the pressure in the 'tank reaches the aforementioned safety rating ofy 325 pounds per square inch and all ofthe stored liquid will be released.

bulk transportation trucks and railway tank cars. By`means of such transportation devices, liquid carbon dioxide can be obtained by bevernge bottling plant operators which is already at a desired subatmospheric temperature which corresponds with the temperature of the liquid stored in the tank i. In other words, liquid carbon dioxide will be delivered in any desired plantities and in a condition where its pressure will. be approximately 300 pounds per square As has been stated above, carbon dioxide willv f only be withdrawn fromthe storage tank 5 in vapor form and this withdrawal will always be through the pipe 8. A manually operable shutoff valve l0 ls provided in this line for controlling the on and olf periods and the rate oi discharge of the vapors. A pressure-operated mercold switch device Il is connected in the line I and will be' subjected to the vapor pressure in the tank` 6 when the vapor control valve il is open, It will be explained at a later point that this mercoid switch il includes two circuit making and breaking devices for one of the systems to be described 'in detail and only one circuit making and breaking device for a modified form ofsystem.

The vapor draw-olf line 8 is connected by suit# `able piping i2 to a strainer il, having a drain Il which is controlled by the valve I8. The strainer Il has connected to its discharge a line il which is connected with the inner tube il of a double tube heat exchanger coil IlB. No detail disclosure of this double tube heat exchanger coil is provided.because it merely consists of the inner tube I1 which is concentrically arranged within the bore of the outerv tube I9. The discharge end of the inner tube I1 is connected to the pipe line 20 which extends to the T-coupling 2|. From this coupling two lines 22 and 23 extend. The pipe line 22 is connected to any suitable number of branch lines 24 which in turn extend to the carbonators of the bottling plant. Coupled in each branch line 24l is a p1 essure regulator 25, Each one of these regulators is manually adjustable and functions to reduce the pressure of the carbon dioxide vapor passing therethrough so that the carbonators will be subjected to the desired, constant vapor pressure. The pipe line 23with its control valve 23',

may be employed for connecting a bank of commercial carbon dioxide cylinders, not shown, to the system in case the bulk storage tank type of supply must be placed out of operation, for some unusualV reason.

It will be explained at a later point that the vapor pressure of the liquid carbon dioxide in the tank 5 will be maintained within a relatively narrow range of low temperatures and pressures during the withdrawal of vapors from the tank for delivery to the carbonators, i. e., a temperature and pressure yrange which is considerably below the 300 pounds per square inch extreme pressure value maintained by the refrigerating coil 1 and its refrigerating machine. However, assuming that the vapor pressure of the liquid will never materially exceed a value of approximately 300 pounds per square inch, the carbon dioxide vapors withdrawn from the tank 5 and delivered to the carbonators will have a temperature which does not exceed the temperature value for the 300 pound vapor pressure. This temperature will be approximately 0 F. As a temperature of around 33 F. is desired in the carbonators, and as the drinking water supplied to the carbonators must be reduced in temperature before delivery to the carbonators, the heat exchanger coil lI8 is employed as a means for The lower end of this outer. tube I9 is connected to a suitable coupling 26 which has joined thereto a pipe line 29. A T-coupling 30 is located in the line 29 for connecting thereto a by-pass 3l. The coupling 30 also connects to the line 29 an extension 32.

A combined shut-on valve and air Vent valve 33 `is coupled in the pipe line 21 while a shut- 01T valve 34 is coupled in the pipe line 32. A ldrain valve 35 is connected to the coupling 28 so as to drain water from the lines 21, 29 and 32, as

well as the outer tube I9 of the heat exchanger coil I8, when such a procedure is desirable. The by-pass line 3| has connected thereina solenoid valve 36 and a manually, controlled throttling valve 31. This by-pass line 3l extends to a suitable drain, or the like, for discharge into a sewer, or other means of disposal.

A by-pass 38 is connected to the upper ends of the pipe lines 21 and 32 and is provided with a shut-offv valve 39. This valve 39 is normally closed so that the ilow of water will be down through the heat exchanger coil I8 and then back up through the pipe lines 29 and 32. However. the valves 33 and 34 can be closed to cut off the ow of water through the heat exchanger coil and the valve 39 may be opened to by-pass the water from the supply line 26 directly to the pipe line 40. When the heat exchanger coil I8 is excluded from the water ilow path, the closing of 'the valve 33 will vent this shut-off portion of the water circuit to the atmosphere and the opening of the drain valve 35 will permit the water to be Withdrawn from the outer tube I9 of the exchanger coil to prevent its freezing. It will be recognized that passage of the water through the heat exchanger coil along with the passage of low temperature carbon dioxide vapors will cause the vapors to absorb heat from the water and thereby raise the temperature of the vapors and lower the temperature of the water.

Therefore, the water flowing through the pipe line 40 will be at a somewhat lower temperature than the water flowing through the pipe line 26 if this water has passed through the heat exchanger IB. The pipe line 40 conducts the partially cooled water to a suitable filter 4I and is discharged therefrom through a line 42. The pipe line 42 has a oat controlled valve 43 connected therein and additionally extends to a point of discharge 44 where the water is caused to ilow downwardly over a cooling coil 45. The water, after passing over the cooling coil 45, is collected in a basin 46 and is delivered to a cold water storage tank 41. With this arrangement, the Water will be delivered to the tank 41 until the level of the water in the tank operates the float 48 to close the valve 43. From the cold water storage tank 41, the water, at the desired uniform low ternperature, is delivered to the carbonators through the pipe line 49.

We now have disclosed the two means employed for lowering the temperature of the water to the desired value for delivery to the carbonators. The rst refrigerating step is accomplished by means of the heat exchanger coil I8. The second refrigerating step is accomplished by means of the cooling coil 45. The low temperature of the discharged carbon dioxide vapors accomplishes partial cooling of the water in the heat exchanger coil I8. The low temperature of the brine of a separate refrigerating circuit is employed for the refrigerating action of the cooling coil 45. This coil has its opposite ends connected to pipe lines 50 and 5I which form a part of said brine circuit, not fully shown.

A oat controlled switch 54 is associated with the cold water storage tank 41. It will be explained at a later point that this switch 54 functions to control the operation of the solenoid valve 36 in the by-pass line, or drain 3|, as well as a brine pump which is connected in the refrigerating circuit that includes the pipe lines 5l) and 5I. In other words, when the float controlled valve 43 is closed, no water passes through the line 42 to the point of discharge 44 onto the cooling coil 45'. The solenoid valve 36 then should be opened so that the water will pass directly to the drain through the pipe line 3|. When no water is being discharged onto the cooling coil 45, it is not necessary to operate the electric motor driven pump for the brine circuit. Therefore, the float controlled switch 54 operates to close the circuits to the solenoid valve 36 and the electric motor tial temperature diiierential with respect to the .tor the brine pump when the water level inthe storage tank 41 is below its predetermined maximum and operates to break the circuits to the solenoid valve It and the motor for the brine pump when the level oi water in the tank 41 is at or above its predetermined maximum, or when the ioat controlled valve t3 is closed.

It has been explained above that when carbon Adioxide vapors are withdrawn from a space containing liquid carbon dioxide and vapors, a proper amount of the liquid will vaporize to take the place oi the withdrawn vapors. This vaporlzatemperature of the liquid carbon dioxidel stored in the tank I. Therefore, the carbon dioxide will absorb heat from the liquid passing through the coil Il.. Y

The three-way valve "is held in the position niustrad in m. i by means er the solenoid Il which has its armature il connected'by a cable l1 to a peripherally grooved pulley 69. A second peripherally'grooved-pulley 69, of greated diameter than the pulley 88. has attached thereto a cable l0 which extends-to and is connected with tion of liquid carbon dioxidel bringsabout a selfcooling or self-refrigerating oi the remaining liquid which is accompanied by lowering of the temperature and pressure of the stored liquid. If the lowering of the temperature and pressure of the stored liquid is permitted to continue for a -suiiicient length of time, the temperature ofl the liquid will be lowered to approximately 70 F. and the pressure will drop to approximately 'l5 pounds per square inch, absolute. At these temperature and pressure values, the liquid carbon dioxide will solidify and n'o more vapors can be withdrawn from the space until sumcient heat is absorbed by the carbon dioxide to eect sublirnation. of the same.

It was pointed out above that a certain amount of heat would be absorbed by theliquid -as a result of leakage of heat through the insulation l of the tank 5. This source o! heat input, theretore, will help to counteract the reirigerating ac,- tion resulting from the withdrawal of4 nothing Y. but carbon dioxide vapors. If the withdrawal' of vapors is at a suiilciently low rate, this source of heat will be adequate to completely'counterl which is connected to the water supply line 2G.

This pipe line 65 hasconnected therein a valve Il which is employed for eithencompletely shutting on the flow oi water through the line 5l or for regulating its rate of ilow. The pipe line II extends to a three-way valve 51. One outlet for the casing oi this three-way valve is connected to a heater coil Il. The remaining end of this coil is connected to aline i9 which is suitably joined with one end oi' a coil l that is located at any suitable level in the liquid space of the carbon dioxide storage tank 5. The remaining end of this coil Il is connected to a pipe line li which leads to a T-coupling 62. One branch of thiscoupling has connected thereto a line which is attached to the second discharge openbranch of the T-coupllng I2 is connected to a line il which leads to .a suitable drain or sewer outlet.

The three-way valve 51 is illustrated in Fig. 1 as being conditioned for allowing the water to ilow through the pipe line 55 into the coilv l! of the heater andfrom this coil into the pipe line 5l which delivers the water to the coil 60 located in the liquid carbon dioxide space oi the storage tank L From this coil 50, the water flows of! through the pipe lines Il and BI to the drain.

,ing of the threeway valve casing 51. The second vthe valve operating arm 1I. A spring I2 also is connected to this valve operating arm 'Il and functions to move the arm substantially 90 when the circuit for the solenoid l! is broken. 'I'herefore, when the spring 12 has operated the threeway valve Il. through its arm 1l. the valve will direct the'water from the branch line il to the branch line Il lfrom which it will now into the drain through the pipe line Il. The three-way v alve Il has a vent, not shown, which is placed in communication with the valve casing. outlet which is connected to the heatercoil Il when the spring 12 positions the valve so that the water will drain from this coil, the pipe line Il, the coil l0, and the pipe line ll through the pipe line Il.

From thcabove description, it will be noted that the three-.way valve l1 operates to either cause city water to new 'through the liquid carbon 4ilitvxide heating coil Il and thento a drain or from the line Il through the pipe lines n and M directly tothe drain without passing through the carbon dioxide heating coil il. Ii' carbon dioxide vapors are being withdrawn irom'the tank i at such a rapid rate that water at its normal city main temperature will not be sumeie'nt to i to 225 pounds per square inch, as the maximum.

rl'hiis provides a margin of 'I5 pounds between the maximum of the operating range and the extreme pressure value of 300 pounds at which the vapor condensing coilfl will come into play. This pound margin or diilerential will permit a plant to be shut down for approximately 60 hours before the input of heat through the insulation t will raise the pressure of the stored carbon dioxide from the 225 pound maximum 0i the operating range to the 300 pound extreme pressure value. A shut-down period of 60 hours will take care oi plants operating on a uve-day week and will allow almost three days time in which to make repairs to the refrlgerating machine connected to the coil l even if the plant is shut down while `the refrlgeratlng machine is being overhauled.

Reference will now'be made to Fig. 3 which diagrammatically illustrates the wiring system The temperature oi the city water, of course, is

considerably above 32 F. and provides a substanand the electric control devices, etc., ior the apparatus `oi Fig. l. The main electrical supply lines of the wiring system are designated by the reference characters 1I, 18, and 1I. These lines are connected to the respective poles or a triple pole. single throw switch TI. Branch lines 1l, 1I,

tf1-sil 2,322,625

and 88 are connected to the main supply lines 14 to 18 to provide a second operating circuit. 'I'hese lines are connected to the three terminals of a second triple pole, single throw switch 8i.

The second set of terminals for the switch 11 have connected thereto the lines 14a, 15a, and 36a which extend to the motor starter 82 for the electric motor 83 which drives the refrigerating machine connected to the condensing coil 1 located in the carbon dioxide storage tank 5. This motor starter 82 operates in response to actuation of the mercoid switch 84 located in the control circuit 85. A manual switch 86 is provided in this control circuit 85 to render the same operative or inoperative. The mercoid switch 84 operates in response to the vapor pressure prevailing in the storage tank 5. For example, when this vapor pressure reaches 300 pounds per square inch, the mercoid switch 84 is actuated to close the control circuit 85 for the motor starter 82 and the electric motor 83 is energized. Operation of this electric motor causes the refrigerating plant connected to the condenser coil 1 to be driven and vapors in the tank will be condensed until the pressure in the tank drops below the 300 pound value which will result in opening the mercoid switch 84.

From the triple pull switch 8|, three'branch lines 18a, 18a, and 88a extend tothe magnetic motor starter 81. Lines 18b,18b. and 88h extend from the motor starter 81 to a manually operable, triple pole, single throw switch 88. Lines 88, 80, and 8| extend from this switch 88 to the electric motor rfor the brine pump. The brine pump motor starter 81 is controlled by the circuit 82 which extends to the oat actuated switch 54, shown in Fig. 1 as being associated with the cold water storage tank 41.. When the water in the tank 41 is below its predetermined maximum level, water is flowing into this tank and the brine pump is driven by its motor as a result of actuation of the float controlled switch 54 and closing of the circuit to the brine pump motor through the starter 81.

The solenoid valve 88, located in the by-pass pipe line 8| has its coil 86a connected by the wire 83 to the branch line 18a. A second wire 84 connects the solenoid coil to the terminal 85 of the normally closed relay 86. The second terminal 81 of this relay is connected by the wire 881 to the branch line lao. It will be apparent, there-I fore, that when the triple pole switch 8| is closed, current will flow through the wires 93 and-84 and the normally closed relay 88 to thesolenoid. valve coil 88a. 'The winding 88 for the relay 96 is connected by the wire |88 to the wire 18h and by the wire |8i to the wire 18b. The winding 88 of the relay 85, therefore, is under the control of the brine pump motor starter 81 and the fioat operated switch 54. In other words, when the float operated switch t8 closes the circuit to the brine pump motor starter 81, it also closes the circuit to the winding 88 of the relay 8B. Energi- `zation of this relay winding 98 breaks the circuit to the solenoid valve coil 36a. When the circuit to the solenoid coil 85a is broken, the solenoidl valve 36 is closed. The drinking water then ows from the heat exchanger coil |8 to the storage tank 41 over the cooling coil 45 and the brine pump is in operation. When the float operated switch 54 breaks the control circuit of the brine pump motor starter 81, the brine pump ceases to operate and the relay winding 88 is de-energized. The circuit through the relay then is closed and the solenoid valve coil a is energized for holding the solenoid valve 36 open.

A second control circuit is connected to the branch lines 14a and 15a which lead to the refrigerator motor starter 82. This second control circuit includes the two mercoid switches ila and ilb which are housed in the pressure operated mercoid switch designated by the reference character in Fig. 1. These mercoid switches ||a and IIb have the windings-|82 and |83 of relays |84 and |85, respectively, connected in their circuits. Current is supplied to the mercoid switch ||a and the relay winding |82 by the branch lines |86 and |81 which extend to the wires 14a and 15a, respectively. A manual control switch |88 is located in the branch line |81. The mercoid switch Hb and the relay winding |88 are supplied with electricity through the branch lines |88 and ||8 which are connected to the wires |86 and |81, respectively.

'The switch of the relay |84 controls the circuit to the winding 18a of the electric `heater 18 which is associated with the water heating coil 58. This circuit for the heater 13a includes the wires I|| and `I |2 which are connected to the control wires 81 and"|06, respectively. The circuit for the winding 65a of the solenoid 65 includes the wire I2, in combination with the heater coil 18a, and the wire H3. The wire ||2 is attached to the control branchline |88, while the wire ||8 is electrically connected to the branch control wire |81.

It will be apparent from the above description that the pressure in the carbon dioxide storage tank 5 determines the operating periods of the solenoid 65 and the electric heater 18 through the medium of the pressure operated mercoid switches Iia and lib. OI course, these two mercoid switches may be set to operate at 'any desired carbon dioxide vapor pressures, but it has been found to be most desirable to have the mercoidswitch a operate at a vapor pressure of 200 pounds per square inch to close the circuit for `the heater coil 13a and to open the circuit to this heater coil when pressures above 200 pounds prevail. It has been determined, also, that the circuit for the solenoid coil 65a. should be closed whenever the vapor pressure in the storage tank 5 is at a value of 225 pounds per square inch, or lower. At pressures above 225 pounds, the circuit for the solenoid 65 should be open.

We now have fully described a system which will operate in the following manner:

Let us assume for some abnormal reason that the bottling plant has been shut down for a period greater than 60 hours. The refrigerating device driven by the electric motor 83 and con-` nected tothe condenser coil 1 has been in operation to maintain the vapor pressure in the storage tank 5 at a value of approximately 300 pounds per square inch.- -When the plant resumes operation, the carbon dioxide vapors withdrawn through the line 8 are at this 30o pound pressure.

'I'his withdrawn vapor passes through the heat exchanger coil 8 to the pressure reducers 25 which operate to lower the pressure of the vapors to the desired value below lilo pounds. Water iiows from the city main, or from a well.

through the pipe line 26 and the line 21 to the heat exchanger I8 and from this heat exchanger through pipe lines 28, 32, 48, and 42 to the point of discharge 44 onto the cooling coil 45. The heat exchanger I8 partially reduces the temperature of this water, while the cooling coil 45 lowers the pipe lines 6|' and Bl.

Il the carbon dioxide vapor pressure still con.

,owing through the coil escasas the water temperature to the desired valueior being delivered to the storage tank 41. From this tank the water flows through the pipe line' ,I9 to the carbonators. During the ow of water over the cooling coil 45, the brine pump is operated. 4

We shall now assume'that vapors are withdrawn from the -tank i at a suillciently rapid rate to cause the pressure in the tank to drop notwithstanding the absorption of heat through the insulation! of thetank. The vapor pressure in the tank 5 will continue to drop until it reaches thevalue of 225 pounds per square I.

inch. At this value, the mercoid switch ||b will be operated to close the circuit for the winding la of the solenoid 8l. The three-way .valve 51 then will be operated by the solenoid 55 for causing water to ilow from'the water line 26 lthrough the pipe line 65, the heater coil 58, 'and the pipe line 59 to the coil 60 located in the carbon dioxide storage tank 5. Fromvthis coil Il, the water is delivered to the drain through tinues to drop and ilnally reaches a value of 200 pounds per square inch, the mercoid switch ||a will be operated-fior closing the circuit ofthe heater coil 13a. Energization oi the coil for the heater 13, see Fig. 1, will cause the water passing through the coil ll to be heated. 'I'he electric heaterv lma'y be oi' lany desired capacity and -may be capable of heating the water passing through vthe coil S8 to any-desired hightemper- Y ature. Thiss'uperheated water then will ilow from the coil 88 through the pipe line vl! tothe coil lll located in the carbon dioxide liquid oi the above 225 pounds so that 'the circuit for the solenoid Q5 will be broken. .The spring 12 will then actuate the three-way valve-i1 for diverting the water flowing through the pipe line 55 to the line C3 and from this line to the drain through the pipeline N.

-above 200 pounds when the heater coil circuit I! the rate 0f Withdrawal of I to the cold water storage tank I1. The reference characters employed in Fig. 1 lor designating certain elements will be employed in Fig. 2 for identifying the same elements. New reference characters will be applied only to new elements.

Therefore, we have, the water supply line 2t connected to the outer tube i9 of the heat exchanger coil il by means of the pipe line 2i which has the combined venting and shut-oil valve $3 located therein. The coupling 2li connected to the lower end of the outer tube i9 has the pipe 29 attached thereto which leads to the coupling 3Q. The pipe line 32 leads from one branch of the coupling 30 to the pipeline te and has the shut-oil valve 3l connected therein. The coupling 30 has a by-pass 3| attached thereto which extends to the inlet for the three-way l valve 51. This byvpass line 3| has connected therein'the solenoid valve 36 and the throttling valve 31.

One branch of the three-way valve 5'i is connect'ed to the water heating coil Bill that has associated therewith the electric heater unit 13. The second discharge branch of the three-way valve '51 has connected thereto the branch pipe line 63, which is shown in Fig. l as extending to the T-coupling 62. The three-way valve 51 has its operating arm 1| which is to be operated' by the solenoid 8l and the spring 12 in the manner illustrated in Fig. l. From the water heater coil Il. the pipe line 59 extends for connection with the coil 60 located in the liquid space of the carbon dioxide storage tank 5. The flow of the carbon dioxide vapors through the heat exchanger coil I8 is by meansof the pipe I6 and the inner tube I1 which connects at its lower end withthe line 2l leading to the pressure reducing valves 2l and the carbonators, not shown.

It is believed to be unnecessary to provide a speciilc illustration of the wiring diagram i'or the modified system of Fig. 2. The solenoid valve ll will be controlled in the same manner by the noat operated switch M so that water will flow through the by-pass line 3| -to the three-'way valve I1 when water isfnot being delivered to the cooling .coil 4I. The solenoid 6l forthe It should be apparent Afrom the above description that the carbon dioxide vapor pressure in l the storage tank B will be maintained within theA relatively narrow range of from 200 pounds to 225 pounds per square inch during' periods of operation of the beverage bottling plant and under normal operating conditions the coil 1 in the storage tank 5 will prevent the vapor pressure in the tank from rising above 300 pounds per square inch pressure during shut-down periods. l

Fig. 2 discloses a slight `modification of a portion oi' the system illustrated in Fis. 1. The dif- -three-way valve operating arm 1| will be openated by the same mercoid switch circuit and relay as is'disclosed in Fig. 3. The electric heater for` the water coil 58 also will be operated by the mercoid switch and relay circuit of Fig. 3, which includesthe switch ||a and therelay winding |02. The only modiiication which might be deemed to be desirable-would be to have the relay 8l control the circuit through the wires lill and y|||1 in addition to controlling the circuit through the winding 30a of the solenoid valve 3l.l In

other words. when the relay winding 8l was energized to break thecircuit tothe winding'lla.

of the solenoid'valve 3l, a circuit could be closed through the wires '|06 and- |81; This couldA be accomplished by placing two contacts above the relay contacts $5 and 91 and having the'relay operated blade engage these two contacts for closing the circuit through the wires lill and |01 when the blade moved out of contact with the terminals l! and I1.

ference betweenthis Fig.,2 system and the Fig. l

system is that the water delivered to the liquid carbon dioxide heating coil comes Afrom the by-pass line 3| instead or'irom the water supply line 2B. That is to say, water is only fed to the heating coil n when the water which passes through the heat exchangercoil i8 is not going Fig. 4 discloses a further modification o! means for heating the liquid carbon dioxide stored in the tank l to counteract the self-refrigerating "action resulting from the withdrawal of vapors v from vthis tank. 4This Fig. e modiilcation consists ofemploying any suitable number of velectric Y heating coils, or elements, Ill in the liquid space of the tank' l. The circuit wires |||a and ||2a may be considered the sameas the wires I'I'i and H2, oi Figli-which lead 'to the electric water heating coil 13a. The mercoid switchl lia'and the relay Ill, therefore, would operate to control v'the' fiowfoi current throu h the electric heating n umts i I4. The. mercoid tch employed for controlling the circuit through the heating elements jm could be set toppers@ so that the circuit' would be closed at va vapor pressure value oi 200 pounds per square inch, and the setting could be such that the merooid switch would open ythe not, therefore, be refrigerated by Fig. illustrates the bulk capacity storage tank 5 for the liquid carbon dioxide with'its insulating covering 6. ,A pipe line III is connectedto the vapor space of the tank l and is employed during charging of the tank with liquid carbon dioxcircuit to the heating elements ill -when the vapor pressureLvalue was- 225 pounds'. a

It will be appreciated "that the electric heating elements IM of the Fig. 4 modiilcation may be employed to either entirelydisplace the heating coil, with all o! its related elements, and the v use of water to raise the pressure of the stored liquid carbon dioxide, orto only displace the. heating coll Il in the 'water` circuit and the electric heater 1I for this latter coil.

It will be appreciated that although the modiilcations of Figs. 2 and 4 only disclose certain porf-v which are not illustrated in Figs. 2 and 4 should be construed as forming a part oft the complete systems for the modiilc'ations of Figs. 2 and 4..

'I'he previously described embodiments oi.' the invention.. and particularLv those illustrated by Pigs. 1 and 2, employ the higher temperature of tions of thesystem completely illustrated in Figs. i' and 3, the elements of these latter two figures `city or vwell ywater to prevent the temperatureo the stored liquid carbon .dioxide from dropping.

below a certain minimum value with its corresponding minimum vapor pressure. .The city or well water is wasted after it has accomplished this desired result. The low temperature oi the carbon dioxide vaporswithdrawn from the sinrage tank is employed in these previous embodiments to partially refrigerate the water going to the carbonators. A mechanical'reirigerator unit is employed for preventing the temperature: and

the pressure or the stored liquid carbondioxlde from rising beyond a pre-selected extreme pressure value "during prolonged shut down periods.

ide to establish communication between the vmpor space' ofthe storage tank land the vaporv space of the tankof the transportation vehicle which is employed for delivering the carbon dioxide to this-bottling plant. The pipe line which is employed for connecting the liquid spaces of.

the two tanks is not shown.

` l A vapor discharge lineV Hi extends'irom the top ofthe storage tank I and is connected to a 'r-coupling Ill. lOne branch of this coupling has a bleeder valve; of suitable construction. III connected thereto .by the short pipe section H9. This bleeder valve'williunction to release carbon dioxide vapors ltoeect self-cooling or self-rei'rigeration of the liquid remaining in the storage tank 5 should other refrigerating means, to be described, fail to'iunction to prevent the vapor pressure of the stored liquid carbon dioxide from rising above a preselected extreme pressure value.

The. remaining branch 'of ther-coupling in .has a pipe line |2l connected thereto; This pipe line leadsto the carbonators of the bottling plant. Pressure( reducing valves, not shown, ot the type designated by the reference character 2l in-Figrl will be incorporated in this line |20 in advance of the carbonatora This pipe line IN, also, may have incorporated therein one of the heat exchanger coils I., shown in Figs.- 1 and 2 'it desired. `A manually' operable shut-on valve |2| isvprovided in the pipe line |20 for control- Final cooling 'of the water going yto the carbonators was obtained by means of a separate or seov ond refrigerating circuit.

' Fig. 5 discloses a further modioation oi the invention in which-the higher temperature of the city or well water, going to the carbonators, is employed for preventing the temperature, andv the v'corresponding vapor pressure, of the stored liquid carbon dioxideffrom dropping below a. -pire-- determined minimum value but the water used for this purpose is not wasted. This extraction ling the on and oi! periods andthe rate of dis-l At suitable points adjecent the bulk storage tank 5, the vapor discharge r pipe line I Zl has connected thereto a high pressure operated switch |22 and a low pressure cpverated switch |23.- These switches are connected in control circuits .which wlllbe dealt with at a charge of the vapors.

later point when the wiring diagram o! Fig. 5 is described.

To prevent the vapor pressure of 'the stored liquid carbon dioxide trom exceeding a preselected extreme pressure value during prolonged shut-down periods of the plant, a cooling coil i is arranged in the vaporspace of the tank l. One

of heat from the city or well water andthe appiication 4of the heat to the stored liquid carbon dioxide; additionally," is employed for eecting refrigeration of the water going to the carbonators. This is accomplished by means of a closed brine circuit which is passed in heat exchange relation with the stored liquid carbon dioxide and the water going to the carbonators. A singie mechanical refrigerator unit is employed in thisfurther modification to perform the dual function of preventing the temperature and vapor pressure of the storedliquid carbon dioxide from rising' above a preselected extreme pressure Y value and for lowering the temperature of the brine in the aforementioned closed circuit when the temperature and pressure of4 the stored liquid carbon dioxide are at such high values that the application of further heat thereto is not desirable and the brine oi' the closedcircuit canbranch of this coil I Zlis connected by thepipe line |25 to the T-coupling |28. One branch of this coupling is connected by the pipe line |21 tothe discharge line of .the mechanical'refrig erator unit |28, which is diagrammatically represented in this ilgure. As this refrigerator unit |28 may be any desired one oi! the numerous mechanical refrigerator units available on' the open market,v and .having the d capacity, it is believed to be'unnecessary to illustrate this unit in detail. The remaining branch of the cooling con |24' has connected4 thereto the pipe seing parecia' heat exchange relation with the stored liquid *carbon dioxide.

From the T-coupling |26 a second pipe line |34 extends to and is connected with one end of the coil |35 located in the heat exchanger |36. The remaining end of this cooling coil |35 ls connected by the pipe line' |31 to the third branch of the T-coupling |30. An electric solenoid operated valve |38 is connected in the pipe line |34 and operates to control the flow of the refrigerant from the unit |28 to the coolingcoil The water to be fed to the carbonators is obtained from the pipe line |39 which may extend from a city water supply main or from some other suitable source, such as an artesian well. The water flows through this pipe line to the point of discharge |40. A float operated control valve |4| is connected in the pipe line |39 and controls the flow of water therethrough. The water discharged from the point |40 ows downwardly over a cooling coil |42 and empties into a collecting basin |43 which delivers the properly refrigerated water to the cold water storage tank |44. Water ilows to this tank until the liquid level therein reaches a predetermined height when the float controlled valve |4| operates to stop the flow. The water, at the desired low temperature, is discharged from the tank |44 through the pipe line |45 which conducts the water tothe carbonators.

If this 'system is operated with the withdrawn vapors from the bulk storage tank passing through a heat exchanger coil I8, see Figs. 1 and 2, the water being delivered to the cold water storage tank |44 may pass through this heat exchanger coil before entering the pipe line |39. As has been explained, the heat exchanger coil |8 is optional equipment with the plant of Fig. 5.

The water cooling coil |42 forms a part of a closed circuit for brine, or the like. This closed circuit includes the pipe line |46 which extends from one end of the cooling coil |42 to the inlet of the brine pump |41. The outlet of this pump is connected to the pipe line |48 which is connected at its remaining end to the inlet opening of the electric solenoid operated three-way valve |49. One'of the two outlets for this three-way valve is connected by the pipe/line |50 to one end of the heating coil |5| which is located at any desired level in the liquid space of the bulk storage tank 5. The remaining end of this heating coil |5| is connected by the pipe line |52 to the remaining endof the water cooling coil |42. When the brine pump |41 is operated and the three-way valve |49 is properly conditioned to connect the pipelines |48 and |50, brine will be circulated through the heating coil |5| in the carbon dioxide storage tank 5 and through the cooling coil |42 for the water discharged at the point |40. The low temperature at which the liquid carbon dioxide is stored in the tank 5 will extract heat from the brine while it passes through the `coil |5i. This extraction of heat by the liquid carbon dioxide will counteract the selfcooling or self-refrigerating effect resulting from the constant withdrawal of vapors through the discharge line H6. The brine, after being cooled by its passage through the coil |5|, will ow up to and pass through the coil |42 where it will extract heat from the water and will effect refrigeration of the latter.

The second discharge opening of the threeway valve |49 has connected thereto the pipe line |53 which empties into the bottom of the heat exchanger space surrounding the refrigerating coil of the unit |36. A second pipe line |54 is connected to the upper portion of the heat exchanger space and extends to the coupling |55 which is connected in the pipe line |52.

During periods when the temperature and pressure of the stored liquid carbon dioxide are at high enough values so as not to require the application of heat to the liquid, the three'way valve |49 will be conditioned to direct the brine flowing from the pump |41 through the pipe line |48 to the pipe line |53. The brine then will flow into the heat exchange space of the unit |36 and out of this space through the pipe li'ne |54 to the line |55 where it will flow up to and through the water cooling coil |42. of the brine flowing through the heat exchanger unit |36 is not low enough to properly refrigerate the waterflowing over the cooling coil |42, the temperature controlled switch |56 will function to actuate the electric solenoid valve |38 for causing the refrigerant of the mechanical refrigerating unit |28 to flow through the heat exchanger coil |35 by way of the pipe lines |34 and |31. This refrigerant will lower the temperature of the brine as'it passes through the coil |35. The mechanical refrigerating unit |28, therefore, will maintain the brine at the desired low temperature when the brine coil |5| in the carbon dioxide storage tank is short circuited out of the brine flow path.

Coming now to the wiring circuits for the various controls, the main supply lines |51, |58 and Y |59 extend to one set of terminals of the manually operablel triple pole, single throw switch |60. The 'remaining terminals of this switch have the wires |510., |580. and |59a connected thereto. These three wires extend to the motor starter |6| f or the electric motor of the mechanical refrigerator unit |28. The three wires for the refrigerator motor are designated by the reference characters |51b, |58b and |59b. The control circuit for the refrigerator motor starter |6| includes the wires |62 and |63 which extend to the pressure switch |32 that is connected to the refrigerant line |3| so as to be influenced by the pressure of the refrigerant flowing through this line. In other words, this refrigerant pipe line |3| extends to the low pressure side of the compressor of the refrigerator unit |28. This pressure switch |32 will operate to close the control circuit for the refrigerator motor starter |6| whenever pressure conditions in the line |3| require refrigerant to be fed to the carbon dioxide storage tank cooling coil |24 or the brine heat exchanger cooling coil |35. This pressure switch |32, additionally, will operate to stop the refrigerator unit |28 when no refrigeration is required in either of the coils |24 or |35.

In fully describing the mode of operation of the system shown in Fig. 1, it was stated that a preselected extreme pressure value of 300I pounds per square inch, gauge, was preferred for the stored liquid carbon dioxide. The high pressure operated switch |22, which is subjected to the vapor pressure in the storage tank 5, therefore, is set to close the circuit for the electric solenoid valve |33 when the vapor pressure in the storage tank 5 reaches this 300 pound value. This control circuit includes the wire |64 which extends from the wire |58a to one side of the pressure switch |22; a second wire |65 which extends from the other side of the pressure switch |22 to one terminal of the coil of the solenoid valve |33, and a third wire |66 which extends from If the temperature the second terminal of the solenoid coil of the valve |33 to the main supply line |59a. When the pressure of the vapor in the storage tank 5 reaches the 300 pound value, the solenoid control valve |33 will be opened and the refrigerant from the refrigerator unit |28 will circulate through the cooling coil |24 to condense vapors in the storage tank 5 and lower the temperature and pressure of the stored liquid carbon dioxide. As was described above, the pressure switch |32 will assure operation ofthe refrigerator unit |28 when refrigerant is required in the carbon dioxide cooling coil4 |24.- The pressure switch |22 will be set to open the circuit tothe solenoid valve |33 vwhenever the temperature and pressure of the stored liquid carbon dioxide have been reduced to any desired values below the aforementioned 300 pound pressure andits corresponding temperature.

Assuming that the system ofFig. 5 should have the narrow operating range for the vapor pressure of the liquid carbon dioxide stored in the tank 5 which was set forth in connection with thesystem of Fig. l; i. e., a minimum pressure of 200 pounds per square inch and a maximum pressure of 225 pounds per square inch, the threeway valve |49 should be automatically operated e to direct the ow of the brine through the heattothe solenoid coil, the valve will be positioned to direct the brine through the coil |5I. When the circuit to the solenoid coil is broken, the valve will be conditioned to direct thebrine to the heat exchange spaceof the heat exchanger unit |36.

. The electric circuit for the low pressure switch |23 and the three-way valve solenoid coil includes the wire |61 which is connected to the main supply wire |58a. The wire |51 has connected theretoa wire |68 which extends to one terminal pf the low pressure switch |23. A wire |69 extends from. the second terminal of this low pressure switch to one terminal of the solenoid coil for the threevway valve |49.. The second terminal of the solenoid coil has the wire |1|| connected thereto and thiswire extends to and is connected with the wire |1I` which extends to the main supply wire It was previously explained that the ilow of the refrigerant from the refrigerating unit |28 through the brine cooling coil was controlled by the temperature switch and the electric solenoid operated valve |33. Circuit wires |12,

connected to the wires |81 and |1i.

The float controlled valve |4| .was previously described as functioning to bring about delivery of refrigerated water to the storage tank |44 when the level of the water in this tank was below a predetermined height and to stop this delivery when the proper'` supply of water is available in this storage tank. When no water is passing over the cooling coil |42, it is not necesescasas invention herewith shown and described are to betaken as preferred examples of the same, and that various changes. in .the shape, size, and arrangement of parts may be resorted to without departing from the spirit of the invention or the scope of the subjoined claims.

What we claim is: 1. A method of conditioning and supplying carbon dioxide to carbonators, comprising estabishing a supply of liquid carbon dioxide in bulk storage in a heat insulating tank, withdrawing onh' carbon dioxide vapors from the supply, raising the temperature of the withdrawn carbon dioxide vapors and delivering the heated vapors t0 the pressure regulators of the carbonators during the entire period of operation of the carbonators, and maintaining the vapor pressure of the carbon dioxide remaining in the supply within a relatively narrow range while the vapors are being withdrawn by applying heat to the carbon dioxide at rates which will balance theself-refrigeration of the carbon dioxide resulting from the withdrawal of vapors.

2. A method of conditioning and supplying carbon dioxide to carbonators, comprising establishing a supply of low temperature liquid carbon dioxide in bulk storage in a heat insulated tank, withdrawing only carbon dioxide vapors from the supply for delivery to the carbonators during the entire period of operation of the carbonators, and

passing a brine in a closed circuit in heat ex 'change relation to the water going to the caring the temperature of the withdrawn vapors and lowering the temperature of the water going to |13 and |14 are provided for this purpose and are the carbonators by passing the4 two in heat exchange relation, delivering the heated vapors to the pressure regulators of the carbonators during the entire period of operation of the carbonators, and maintaining the vapor pressure of the carbon dioxide remaining in the supply within a relatively narrow range while the vapors are being withdrawn by applying heat to the carbon dioxidel at rates which will balance the self-refrigeration of the carbon dioxide resulting from the with drawal of the vapors.

4. A method of conditioning and supplying carbon dioxide to carbonators, comprising estab` lishing a supply of low temperature liquid carbon dioxide in bulk storage in a heat insulated tank, withdrawing only carbon dioxide vapors from the supply, raising the temperature of the withdrawn carbon dioxide vapors and delivering the heated vapors to the pressure regulators of the carbonators during the entire period of operation of the carbonators, and passing a refrigerant in a ci circuit in heat exchange relation to the water gooxide in bulk storage in a heat insulated tank, withdrawing only carbon dioxide vapors from the supply, raising the temperature of the withdrawn 4vapors and lowering the temperature of the water going to the carbonators by passing the two in heat exchange relation, delivering the heated vapors to the pressure regulators of the carbonators during the entire period of operation of the carbonators, and passing a refrigerant in a closed circuit in heat exchange relation to the water going to the carbonators and the liquid carbon dioxide remaining in the supply to eiect further refrigeration of the water and to apply heat to the carbon dioxide to counteract the self-refrigeration of the latter resulting from the with-l drawal of vapors.

6. A method of conditioning and supplying carbon dioxide to carbonators, comprising establishing a supply of low temperature liquid carbon dioxide in bulk storage in a heat insulated tank, withdrawing only carbon dioxide vapors from the supply for delivery to the carbonators during the entire period of operation of the carbonators, passing a brine in a closed circuit in heat exing a supply of low temperature liquid carbon dichange relation to the water going to the carbonators and the liquid carbon dioxide remaining in the supply to effect refrigeration of the water and to apply heat to the carbon dioxide to counteract the self-refrigeration of the latter resulting from the withdrawal of vapors, by-passing the brine around the carbon dioxide in the supply when heating thereof is not required, and flowing the by-passed brine in heat exchange relation with another cooling medium sothat the brine can continue to refrigerate the water.

7. A method of conditioning and supplying .carbon dioxide to carbonators, comprising establishing a supply of low temperature liquid carbon dioxide in bulk storage in a heat insulated tank, withdrawing nnly carbon dioxide vapors from the supply, raising the temperature of the withdrawn carbon dioxide vapors and delivering the heated Vvapors to the pressure regulators of the carbonators during the entire period of operation of the carbonators, passing a brine in a closed circuit in heat exchange relation to the water going to the' carbonators and the liquid carbon dioxide remaining in the supply to efectrefrlgeration oi the water and to apply heat to ,the carbon dioxide to counteract the self-refrigeration of the latter resulting from the withdrawal of vapors, by-passlng the brine around the carbon dioxide in the supply when heating thereof is not required, and ilowlng the by-passed brine in heat exchange relation with another cooling medium so that the brine can continue to refrigerate the water.

8. A method of conditioning and supplying carbon dioxide to carbonators, comprising establishing a supply of low temperature liquid carbon dioxide in bulk storage in a heat insulated tank, withdrawing only carbon dioxide vapors from the supply, raising the temperature of the withdrawn vapors and lowering the temperature of the water going to the carbonators by passing the two in heat exchange relation, delivering the heated vapors to the pressure regulators of the carbonators during the entire period of operation of the carbonators, passing a brine ln a closed circuit in heat exchange relation to the water going to the carbonators and the liquid carbon dioxide remaining in the supply to eiect further refrigeration of the water and to apply heat to the carbon dioxide to counteract the self-refrigeration of the latter resulting from the withdrawal of vapors, by-passing the brine around the carbon dioxide in the supply when heating thereof is not required, and flowing theby-passed brine in heat exchange relation with another cooling medium so that the brine can continue to refrigerate the water.

9. yA method of conditioning and supplying carbon dioxide to carbonators. comprising establishing a supply of liquid carbon dioxide in bulk storage in a heat insulated tank, withdrawing only carbon dioxide vapors from the supply for delivery to the carbonators during the entire operating period of the carbonators, and maintaining the vapor pressure of the carbon dioxide remaining in the supply within a relatively narrow range while the vapors are being withdrawn by passing a liquid, having a higher temperature than the stored liquid carbon dioxide, in heat'exchange relation tothe liquid carbon dioxide while the vapor pressure is between certain values and by applying additional heat to the said higher temperatured liquid, prior to its passage in heat exchange relation with the stored carbon dioxide, When the vapor pressure falls below said certain values.

10. A method of conditioning and supplying carbon dioxide to carbonators, comprising establishing a supply of liquid carbon dioxide in bulk storage in a heat insulated tank, withdrawing only carbon dioxide vapors from the supply.

raising the temperature of the withdrawn carbon dioxide vapors and delivering the heated vapors to the pressure regulators of the carbonators during the entire period of operation of the carbonators, and maintaining the vapor pressure of the carbon dioxide remaining in the supply within a relatively narrow range while the vapors are being withdrawn by passing a lquid, having a higher temperature than the stored liquid carbon dioxide, in heat exchange relation to the liquid carbon dioxide while the values.

vapor pressure is between certain values and by applying additional heat to the said higher temperature liquid, prior to its passage in heat exchange relation with the stored carbon dioxide, when the vapor pressure falls below said certain 11. A method carbon dioxide to carbonators, comprisingl establishing a supply of liquid carbon dioxide in bulk storage in a heat insulated tank and at a preselected subatmospheric temperature and its change relation to water going to the carbonators and the liquid carbon dioxide remaining in the supply to effect refrigeration of the water and to apply heat to` the carbon dioxide, preventing a rise in carbon dioxide vapor pressure beyond a predetermined extreme pressure value which is above the maximum value of the aforesaid range, during any given period when theamount of conditioning and supplying.

of vapors withdrawn from the tank is not suflicient to maintain the vapor pressure within said `relatively narrow range, by flowing a refrigerant in heat exchange relation to the carbon dioxide, by-passing the brine around the carbon dioxide in the supply when heating of the carbon dioxide is not required and ilowing the bypassed brine in heat exchange relation to the aforesaid refrigerant for the carbon dioxide so that the brine can continue to refrigerate the water. v

12. A method of conditioning and supplying carbon dioxide to carbonators, comprising establishing a supply of liquid carbon dioxide in bulk storage in a heat insulated tank, withdrawing only carbon dioxide vapors from the supply, raising the temperature of the. withdrawn vapors and lowering the temperature ofthe Water going to the carbonators by passing the two in heat exchange relation, delivering the heated vapors to the pressure regulators of the carbonators during the -entire period of operation of the carbonators, and Amaintaining the vapor pressure of the carbon dioxide remaining in the l peratured liquid, prior to its passage in heat ex# change relation with the stored carbon dioxide, when the vapor pressure falls below said certain values,

13. A method of conditioning and supplying carbon dioxide to carbonators, comprising establishing a supply of liquid carbon dioxide in bulk storage in a heat insulated tank and at a preselected subatmospheric temperature and its corresponding vapor pressure, withdrawing only carbon dioxide vapors from the supply, raising the temperature of the withdrawn carbon dioxide vapors and delivering the heated vapors to the pressure regulators of the carbonators during the entire period of operation of the carbonators, and maintaining the vapor pressure of the carbon dioxide remaining in the supply Within a relatively narrow range while the vapors are being withdrawn by applying heat to the carbon dioxide in varying amounts in response, to variations in the vapor pressure of the supply to thereby,1 balance the self-refrigeration of the carbon dioxide resulting from the withdrawal of the vapors.

14. A method of conditioning and supplying carbon dioxide to carbonators, comprising establishing a supply of liquid carbon dioxide in bulk storage in a heat insulated tank and at a pre-selected subatmospheric temperature and its corresponding vapor pressure, withdrawing only carbon dioxide vapors from the supply, raising the temperature of the withdrawn vapors and lowering the temperature of the water going to the carbonators by passing the two in heat exchange relation, delivering the heated ,the vapors are being withdrawn by applying heat to the carbon dioxide in Varying amounts in response to variations in the vapor pressure of the supply to thereby balance the self-refrigeration of the carbon dioxide resulting from the withdrawal of the vapors.

15. A method of conditioning and supplying carbon dioxide to carbonators, comprising establishing a supply of liquid carbon dioxide in bulk storage in a heat insulated tank and at' a preselected subatrnospheric temperature and its corresponding vapor pressure, withdrawing only carbon dioxide vapors from the supply for delivery t0 the carbonators during the entire operating period of the carbonators, and maintaining the vapor .pressure of the carbon dioxide remaining in the supply within a relatively narrow range while the vapors are being withdrawn by passing a liquid, having a higher temperature than the stored liquid carbon dioxide, in

.heat exchange relatonto the liquid carbon dioxide while the vapor pressure is between certain Values and by applying additional heat to the said higher temperatured liquid, prior to its passage in heat exchange relation with the stored carbon dioxide, when the vapor pressure falls below said certain values.

16. Apparatus for conditioning and supplying carbon dioxide to carbonators, comprising a heat insulated bulk storage tank for liquid carbon dioxide, -a vapor draw-off line extending from the tank to pressure regulators for the carbonators, a line for supplying water to the carbonators, a single heat exchange device connected in .said vapor draw-off line and said water supply line for eiecting the transfer of heat from the water to the vapors, a heating coil in the storage space of the tank, means for flowing through the heating coil fluid having a higher temperature than the temperature of the carbon dioxide stored in the tank, and control means operating in response to pressure variations in the tank for controlling the flow of the uid through the heating coi1.`

' 17. Apparatus for conditioning and supplying carbon dioxide to carbonators, comprising a heat insulated bulk storage tank for liquid carbon dioxide, a vapor draw-01T line extending from said tank to the pressure regulators of carbonators, a line for supplying water to the carbonators, a single heat exchange device connected in said vapor draw-off line and said water supply line for effecting the transfer of heat from the water to the Vapor, an electric heater element positioned within the storage space of the tank, and control means operating in response to variations in vapor pressure in the storage tank for turning on and off the supply of current to the heating element.

18. A method of conditioning and supplying carbon dioxide to carbonators, comprising establishing a supply of low temperature liquid carbon dioxide in bulk storage in a heat insulated tank, withdrawing only carbon dioxide vapors from the supply for delivery to the carbonators during the entire period of operation of the carbonators, and lowering the temperature of the water going to the carbonators and raising the temperature of the liquid carbon dioxide remaining in the supply, to counteract the self-refrigeration of the latter resulting from the withdrawal of vapors, by effecting the transfer of heat from the water to the liquid carbon dioxide.

v19. A method of conditioning and supplying carbon dioxide to carbonators, comprising establishing a supply of liquid carbon dioxide in bulk storage in a heat insulated tank, withdrawing only carbon dioxide vapors from the supply, raising the temperature of the withdrawn vapors and lowering the temperature of the water going to the carbonators by passing the two in heat exchange relation, delivering the heated vapors to the pressure regulators of the carbonators during the entire period of operation of the carbonators, and maintaining the vapor pressure of the carbon dioxide remaining in the supp15,1 within a relatively narrow range while the vapors are being Withdrawn by periodically diverting the water from its flow to the carbonators and flowing it in heat exchange relation to the carbon dioxide to counteract the self-refrigeration of the latter resulting from the withdrawal of vapors.

20. A method of'conditioning and supplying carbon dioxide to carbonators, comprising establishing a supply of liquid carbon dioxide in bulk storage in a heat insulated tank, withdrawing only carbon dioxide vapors from the suppy `for delivery to the carbonators during the entire operating period of the carbonators, and maintaining the vapor pressure of the` carbon dioxide remaining in the supply below a predetermined maximum value and above the pressure at which the liquid carbon dioxide will solidify, while thevapors are being withdrawn, by ilowing a higher temperatured liquid in heat exchange relation to the liquidl carbon dioxide whenever the vapor pressure is below said maximum value and by raising the temperature of the said higher temperatured liquid above its normal value, prior to its passage in heat exchange relation with the stored carbon dioxide, whenever the vapor pres- A a line for supplying water to the carbonators, a

single heat exchange device connected in said vapor draw-oil? line and said water supply line for effecting the transfer of heat from the water to the vapors, a heating coil'in the storage space of the tank, a cooling coil in the path of flow of vthe water going to the carbonators, -said heating and cooling coils being interconnected for the iiow therethrough of a single medium which will transfer heat from the water to the liquid carbon dioxide in the tank, and means for establishing and stopping the circulation of said medium through said heating coil.

22, Apparatus for conditioning and supplying carbon dioxide to carbonators, comprising a heat insulated bulk storage tank for liquid carbon dioxide, a vapor draw-01T line extending from the tank to pressure regulators for the carbonators, a line for supplying water to the carbonators, a single heat exchange device connected in said Vapor draw-off line and said water supply line for effecting the transfer of heat from the water to the vapors, a heating coil in the storage space of the tank, a cooling coil in the path of flow of the water going to the carbonators, said heating and cooling coils being interconnected for the ow therethrough of';a single medium which l will transfer heat from the water to the liquid carbon 

